US3338793A - Method for production of l-glutamic acid by microbacteria - Google Patents
Method for production of l-glutamic acid by microbacteria Download PDFInfo
- Publication number
- US3338793A US3338793A US397629A US39762964A US3338793A US 3338793 A US3338793 A US 3338793A US 397629 A US397629 A US 397629A US 39762964 A US39762964 A US 39762964A US 3338793 A US3338793 A US 3338793A
- Authority
- US
- United States
- Prior art keywords
- culture
- culture medium
- glutamic acid
- amine
- strain
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- JYJIGFIDKWBXDU-MNNPPOADSA-N inulin Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)OC[C@]1(OC[C@]2(OC[C@]3(OC[C@]4(OC[C@]5(OC[C@]6(OC[C@]7(OC[C@]8(OC[C@]9(OC[C@]%10(OC[C@]%11(OC[C@]%12(OC[C@]%13(OC[C@]%14(OC[C@]%15(OC[C@]%16(OC[C@]%17(OC[C@]%18(OC[C@]%19(OC[C@]%20(OC[C@]%21(OC[C@]%22(OC[C@]%23(OC[C@]%24(OC[C@]%25(OC[C@]%26(OC[C@]%27(OC[C@]%28(OC[C@]%29(OC[C@]%30(OC[C@]%31(OC[C@]%32(OC[C@]%33(OC[C@]%34(OC[C@]%35(OC[C@]%36(O[C@@H]%37[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O%37)O)[C@H]([C@H](O)[C@@H](CO)O%36)O)[C@H]([C@H](O)[C@@H](CO)O%35)O)[C@H]([C@H](O)[C@@H](CO)O%34)O)[C@H]([C@H](O)[C@@H](CO)O%33)O)[C@H]([C@H](O)[C@@H](CO)O%32)O)[C@H]([C@H](O)[C@@H](CO)O%31)O)[C@H]([C@H](O)[C@@H](CO)O%30)O)[C@H]([C@H](O)[C@@H](CO)O%29)O)[C@H]([C@H](O)[C@@H](CO)O%28)O)[C@H]([C@H](O)[C@@H](CO)O%27)O)[C@H]([C@H](O)[C@@H](CO)O%26)O)[C@H]([C@H](O)[C@@H](CO)O%25)O)[C@H]([C@H](O)[C@@H](CO)O%24)O)[C@H]([C@H](O)[C@@H](CO)O%23)O)[C@H]([C@H](O)[C@@H](CO)O%22)O)[C@H]([C@H](O)[C@@H](CO)O%21)O)[C@H]([C@H](O)[C@@H](CO)O%20)O)[C@H]([C@H](O)[C@@H](CO)O%19)O)[C@H]([C@H](O)[C@@H](CO)O%18)O)[C@H]([C@H](O)[C@@H](CO)O%17)O)[C@H]([C@H](O)[C@@H](CO)O%16)O)[C@H]([C@H](O)[C@@H](CO)O%15)O)[C@H]([C@H](O)[C@@H](CO)O%14)O)[C@H]([C@H](O)[C@@H](CO)O%13)O)[C@H]([C@H](O)[C@@H](CO)O%12)O)[C@H]([C@H](O)[C@@H](CO)O%11)O)[C@H]([C@H](O)[C@@H](CO)O%10)O)[C@H]([C@H](O)[C@@H](CO)O9)O)[C@H]([C@H](O)[C@@H](CO)O8)O)[C@H]([C@H](O)[C@@H](CO)O7)O)[C@H]([C@H](O)[C@@H](CO)O6)O)[C@H]([C@H](O)[C@@H](CO)O5)O)[C@H]([C@H](O)[C@@H](CO)O4)O)[C@H]([C@H](O)[C@@H](CO)O3)O)[C@H]([C@H](O)[C@@H](CO)O2)O)[C@@H](O)[C@H](O)[C@@H](CO)O1 JYJIGFIDKWBXDU-MNNPPOADSA-N 0.000 description 1
- 229940029339 inulin Drugs 0.000 description 1
- 239000008101 lactose Substances 0.000 description 1
- 239000000594 mannitol Substances 0.000 description 1
- 235000010355 mannitol Nutrition 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 238000013048 microbiological method Methods 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 208000030194 mouth disease Diseases 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- UPHWVVKYDQHTCF-UHFFFAOYSA-N octadecylazanium;acetate Chemical compound CC(O)=O.CCCCCCCCCCCCCCCCCCN UPHWVVKYDQHTCF-UHFFFAOYSA-N 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 229940056360 penicillin g Drugs 0.000 description 1
- 229940056367 penicillin v Drugs 0.000 description 1
- 150000002960 penicillins Chemical class 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- BPLBGHOLXOTWMN-MBNYWOFBSA-N phenoxymethylpenicillin Chemical compound N([C@H]1[C@H]2SC([C@@H](N2C1=O)C(O)=O)(C)C)C(=O)COC1=CC=CC=C1 BPLBGHOLXOTWMN-MBNYWOFBSA-N 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- HEBKCHPVOIAQTA-ZXFHETKHSA-N ribitol Chemical compound OC[C@H](O)[C@H](O)[C@H](O)CO HEBKCHPVOIAQTA-ZXFHETKHSA-N 0.000 description 1
- NGFMICBWJRZIBI-UJPOAAIJSA-N salicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1CO NGFMICBWJRZIBI-UJPOAAIJSA-N 0.000 description 1
- 229940120668 salicin Drugs 0.000 description 1
- CDAISMWEOUEBRE-UHFFFAOYSA-N scyllo-inosotol Natural products OC1C(O)C(O)C(O)C(O)C1O CDAISMWEOUEBRE-UHFFFAOYSA-N 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- SITVSCPRJNYAGV-UHFFFAOYSA-L tellurite Chemical compound [O-][Te]([O-])=O SITVSCPRJNYAGV-UHFFFAOYSA-L 0.000 description 1
- CWERGRDVMFNCDR-UHFFFAOYSA-M thioglycolate(1-) Chemical compound [O-]C(=O)CS CWERGRDVMFNCDR-UHFFFAOYSA-M 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P13/00—Preparation of nitrogen-containing organic compounds
- C12P13/04—Alpha- or beta- amino acids
- C12P13/14—Glutamic acid; Glutamine
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S435/00—Chemistry: molecular biology and microbiology
- Y10S435/813—Continuous fermentation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S435/00—Chemistry: molecular biology and microbiology
- Y10S435/8215—Microorganisms
- Y10S435/822—Microorganisms using bacteria or actinomycetales
Definitions
- This invention relates to a method of cultivating bacteria belonging to Microbacterium ammoniaphilum areobically in a nutrient culture medium having molasses as the main component, and thereby accumulating an appreciable amount of L-glutamic acid in said culture medium.
- object of this invention is to provide L-glutamic acid ammoniaphilum belonging to the new species, and the second characteristic feature lies in adding surface active agents selected respectively from the first and the secondcomponent chemical agents in two steps at an appropriate time in order to normally carry out the production of L- glutamic acid by fermentation.
- Agar colonies Growth be fairly late, after 24 hrs. makes colonies having 0.5-1 mm. of dia., after duration in the culture increase the magnitude, colonies: small cir- 3,338,793- Patented Aug. 29, 1967 ice cle, edge: entire, slightly raised, surface: slightly dryish-smooth, opaque, and lemon yellow which increases with ageing.
- Agar stab and Thioglycollate medium stab grow only on surface, aerobic.
- Nutrition-requesting nature biotin-requesting and cystine.
- the strain Microbacterium ammoniaphilum belonging to the order Eubacteriales because the strain is a bacterium of which characters are the following, i.e., gram strain: positive, spore formation: none, acid-fast strain: negative, hight pleomorphism, angular and palisade: observed clearly.
- the family Micrococcuseae is coccoi or egg-shaped having no thermal-resistance, the family Brevibacteriace-ae has no pleomorphism and no thermal-resistance and the family Baccilluseae has spore formation, it is concluded that the strain of the invention belongs to none of the above families and that the strain of the invention should belong to the family Corynebacteriaecae. And further, it is clearly concluded from the following facts (1)-(7) in careful comparison with genuses belonging to the family of Corynebacteriaecae cited in Bergeys Manual that the strain of the invention should belong to the genus Microbacterium.
- Step Addition 2 Step Addition Name of Surface Active Agents Amount of Amount of Amount Time of Ad- L-Clutamic Amount Time of Ad- L-Glutamic added (g./dl.) dition (hrs) Aznd paired added ⁇ g.ldl.) dition (hrs.) Acid formed 8- I11 (mg/m1.)
- the strain produces lactic acid in a medium in a stand culture.
- the species of the invention differs from both Microbacterium lacticum and Microbacterium flavum which are described as species belonging to the genus Microbacterium in Bergeys Manual, in view of the difference in the starch and maltose decomposition natures which-are considered as the identification key of the both species.
- both Microbacterium lacticum ATCC No. 8180 and Microbacterium flavum ATCC No. 10340 which have been deposited as a standard strain belonging to the genus Microbacterium at the American Type Culture Collection and have been given the numbers, have no ability of producing L-glutamic acid.
- the strain of the invention has a Composition of culture medium for the main fermentation:
- the method of this invention based on the two-step addition system, as compared with the hitherto-known methods based on the one-step addition system, makes it possible to appreciably increase the formation of L-glutamic acid and, what is more, to make the amount of chemical agents to be added small, and, therefore, there is the advantage that the method of this invention can be worked economically on a commercial basis.
- chemical agents are added in two steps to a culture medium or to the medium under cultivation.
- the chemical agents to be added in the first step there are non-ionic surface active agents, which are selected from the group consisting of esters of polyoxyethylene sorbitan fatty acid, polyoxyethylene fatty acid, etc. and polyoxyethylene alkylamine.
- the chemical agents to be added in the second step are selected from the group of compounds such as surface active agents and 5 antibiotics. The use of chemical agents having the components shown below is particularly effective.
- Components of the chemical agents to be added in the econd step Lauryl amine, Stea-ryl amine, palmityl amine, alkyl trimethyl ammonium chloride, alkyl dimethyl benzyl ammonium chloride, penicillin, erythromycin, leucomycin, synthetic penicillin derivative, streptomycin, etc.
- those which are used in the first step are added within several hours after commencement of culture, that is, at the time when the difference shows -0.6 between the optical density, as in the case in which the twenty-times diluted culture broth is measured with a wave length of 655111, by using an ordinary photoelectric colon'meter with a 10 mm. cell, and the optical density at the time the culture is commenced.
- those which are used in the second step are added after lapse of more than one hour from the time the first component was 'added.
- the above-mentioned difference in optical density at this time is preferably 0.4-1.0
- the molasses referred to herein is cane molasses.
- the strain used in this invention a typical one of which is ATCC 15354 strain, has several color mutants, which have the same characteristic features in taxology as those mentioned above. Accordingly, the strain which is made the objective of this invention is fully effective, regardless of whether its mutant is natural or artificial.
- the first-component surface active agent one having polyoxyethylene monopalmitate as the main component was. selected and, When the optical density of the culture medium measured by the aforesaid method was 0.3, i.e. after about 5 hours from the time the culture was commenced, it was added to the culture medium so that the concentration thereof became 0.1 g./dl. And, as the second-component surface active agent, one having lauryl amine as the main component was taken up and, in the 6th hour after commencement of culture when the optical density became 0.55, it was added to the culture medium so that the concentration thereof became 0.025 g./dl.
- the pH of the culture medium under cultivation was adjusted to 7-8 with ammonia gas. While the culture temperature was being maintained at 30 C., about 2.6 l. of a liquid of cane molasses having a carbohydrate concentration of 50 g./dl. was supplied from the 12th hour after commencement of culture so that the concentration of the remaining carbohydrate became 1 g./d1., and the culture was carried out for 36 hours. In the culture medium, there was observed the accumulation of L- glutamic acid with a concentration of 7.85 g./dl. The total amount of L-glutamic acid formed was 1015 g. and the amount of carbohydrate used was 1989 g.; that is, the rate of yield was 51%.
- the concentration of L-glutamic acid was 1.85 g./dl., and the total amount of L-glutamic acid formed was only 225 g.
- 795 g. of coarse L-glutarnic acid crystals was obtained by the usual method from the former fermentation liquid.
- EXAMPLE 2 The culture was carried out in the same way as in Example 1 by using the same Microbacterium ammoniaphilum ATTCC 15354 as in Example 1. However, the main fermentation culture medium used was of the following composition.
- composition of the main fermentation culture medium is composition of the main fermentation culture medium
- the pH adjustment and the supply of carbohydrate were carried out in the same way as in Example 1, but as the first-component surface active agent, one having polyoxyethylene sorbitan monopalmitate as the main component was used; it was added to the culture medium so that the concentration thereof became 0.1 g./d*l. in the 4th hour after commencement of culture when theoptical density of the culture medium was 0.3. Also, as the second component, a surface active agent'having lauryl amine as the main component was added to the culture medium so that the concentration thereof became 0.025 g./dl. when the optical density was 0.60, i.e. after lapse of 5.5 hours from the time the culture was commenced, and the culture was continued for 36 hours.
- the first-component surface active agent one having polyoxyethylene sorbitan monopalmitate as the main component was used; it was added to the culture medium so that the concentration thereof became 0.1 g./d*l. in the 4th hour after commencement of culture when theoptical density of the culture medium
- EXAMPLE 3 1.5 ml. of the culture broth pre-cultured by using the same Microbacterium ammoniaphilum ATCC 15354 as in Example 1 was inoculated into 75 ml. of the culture medium having the following composition placed in a 500 ml. shaking flask.
- a surface active agent having palmityl amine as the main component was added as the second component in a ratio of 0.015 g./dl., and the culture was carried out for 48 hours at 30 C.
- the culture medium there was observed the 7 accumulation of L-glutamic acid with a concentration of 3.2 g./dl.
- the second component when the second component was not added, there was the accumulation of L- glutamic acid with a concentration of only 1.5 g./dl.
- a surface active agent having benzalkonium chloride as the main component was added at a ratio of 0.01 g./dl. to the culture medium.
- the analytical values of the cane molasses medium after 48 hours there was observed the accumulatreated with ammonium phosphate used herein were as tion of L-glutamic acid with a concentration of 2.7 g./dl. follows: against this, when the second component was not added, there was observed the formation of L-glutamic acid with TQtal carbohydrate 1607 a concentration of only 0.8 g./ d1.
- Cane molasses 10 In the 6th hour after commencement of culture, a sec- 30 2 4 ond-com'ponet surface active agent having alkyl trimethyl polyoxyethylehe sorhltan monopalmltate (Tween ammonium chloride as the main component was added 02 to the culture medium so that the amount thereof became In the 8th hour ft commencement f culture, various g In the culture h h after f i there antibiotics were added.
- Penicillin G 5 25 s 20 U/ml 15.0 Phenoxypenieillin 5 U/rnl 21.4 20 U/ml 14.6 Penicillin v. 5U/rul 25.9 20 U/ml 15.1 Tetracyelin 5mog./ml 14.7 10 mcg./ml 2.4 Erythromyein lmcgJml. 14.2 10 mcgJmL- 5.0 Leuicomycin 0.5 meg/ml. 18.8 5mcg./ml 7.7
- amine as main component 1 g. of stearylamine acetate Catiolite 500 ml. of the bacterial seed of Microbacterium ammoniaphilum ATCC 15354 obtained in the same way as in Example 6 was inoculated into 10 l. of the culture medium (charged in 20 l. jar fermenter) for the main fermentation having the following composition:
- Cane molasses (as total carbohydrate) l0 KH PO 0.1 Polyoxyethylene sorbitane monopalmitate (Tween In the 9th hour after commencement of culturing 3.0 SA) was added. The culture was carried out under submerged aerobical conditions while adjusting the pH to 8.0 with ammonium liquid during culturing. The amount of L-glutamic acid ac cumulated in the cultue medium after 48 hrs. was 46.0
- L-glutamic acid can be collected from the culture broth in the same way as in Example 1.
- EXAMPLE 8 Like in Example 6, Microbacteriwm ammoniaphilum ATCC 15354 was shake-cultured at 30 C. in a seed culture medium, and 500 ml. thereof was inoculated into a 20 l. jar fermenter containing l. of the culture medium for main fermentation having the following composition:
- an improvement comprising carrying out said fermentation in the presence of a nonionic surface active agent selected from the group comprising polyoxyethylene sorbitan monopalimitate, polyoxyethylene sorbitan monostearate polyoxyeth ylene monostearate, polyoxyethylene monopalmitate and polyoxyethylene alkylamine, subsequently adding a chemical agent selected from the second group comprising lauryl amine, stearyl amine, palmityl amine, alkyl trimethyl amine chloride, benzalconium chloride, penicillin, erythromycin, leucomycin streptomycin to the culture medium, continuing the culture aerobically, thereby forming and accumulating L-glutamic acid in the culture medium and isolating and collecting the same.
- a nonionic surface active agent selected from the group comprising polyoxyethylene sorbitan monopalimitate, polyoxyethylene sorbitan monostearate polyoxyeth ylene monostearate, polyoxyethylene monopalmitate and polyoxyethylene alkylamine
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Description
United States Patent 3,338,793 METHOD FOR PRODUCTION OF L-GLUTAMIC ACID BY MICROBACTERIA Sotno Yamamoto, Tetsukazu Goto, and Takeyoshi Ohsawa, Nobeoka-shi, Miyazaki-ken, Japan, assignors to Asahi Kasei Kogyo Kabushiki Kaisha, Osaka, Japan No Drawing. Filed Sept. 18, 1964, Ser. No. 397,629
3 Claims. (Cl. 195-47) This invention relates to a method of cultivating bacteria belonging to Microbacterium ammoniaphilum areobically in a nutrient culture medium having molasses as the main component, and thereby accumulating an appreciable amount of L-glutamic acid in said culture medium. The
object of this invention is to provide L-glutamic acid ammoniaphilum belonging to the new species, and the second characteristic feature lies in adding surface active agents selected respectively from the first and the secondcomponent chemical agents in two steps at an appropriate time in order to normally carry out the production of L- glutamic acid by fermentation.
Hereunder, a detailed statement is given as to a typical strain, which has a strong ability to produce L-glutamic acid, of the Microbacterium ammoniaphilum mentioned in the first characteristic feature above. This strain was deposed with the American Type Culture Collection under date of Feb. 12, 1964, and has been recorded as ATCC No. 15354. In the testing of said strain, the same microscopic observation as in the Manual of Microbiological Methods by the Society of American Bacteriologists (1957) was followed to obtain the following results. (I) Microscopic observation:
(1 Morphological characteristics Vegetative cells: rods; usually 0.6-0.8 x 1.0-2.5,u;
slight Pleomorphism; in one scope, observed clubshape, slightly curved and swollen; observed angular, palisade and Chinese letter based on a snapping division; not observed branching; not observed life cycle or bud formation in each age of fermentation.
(2) Gram stain: positive, not change the dyeability in each ago of fermentation.
(3) Spore formation: none (4) Flagella: none (5) Small granules (Refrels or Alberts method): ob-
served clearly at both poles of cell, in some cases observed at only one pole.
( 6) Motility: none.
(7) Acid-fast stain: negative.
(II) Cultural characteristics:
(1) Agar colonies Growth: be fairly late, after 24 hrs. makes colonies having 0.5-1 mm. of dia., after duration in the culture increase the magnitude, colonies: small cir- 3,338,793- Patented Aug. 29, 1967 ice cle, edge: entire, slightly raised, surface: slightly dryish-smooth, opaque, and lemon yellow which increases with ageing.
(2) Agar stroke Growth: Excellent.
Form of growth: Filiform. Odour: Absent.
Colour of medium: Unchanged.
(3) Agar stab and Thioglycollate medium stab: grow only on surface, aerobic.
(4) Nutrient broth: moderate growth with formation of membranous sediment after growth, odourless.
(5) Blood agar: hemolytic creaction: none.
(6) Lofller medium: abundant growth.
(7 Blood tellurite medium: black colonies.
(8) Potato medium: colonies: lemon yellow from initial culture. (III) Physiological characteristics:
(1) Temperature relations:
Optimum temperature: 25-35 C. Thermal resistance: survives for /2 hour at C.
and hour at 72 C. in skim-milk culture.
(2) Catalase reaction: positive.
( 3) Nitrite production from nitrate: none.
(4) Production of hydrogen sulfide: none.
(5) Indol production: negative.
( 6) M.R. reaction: positive.
(7) V.P. reaction: negative.
( 8) Growth in Kosers medium: none.
(9) Growth in Huckers medium: none.
(10) Urease: positive.
( ll) Gelatin stab: none.
(12) Hydrolysis of starch: none.
( 13) Litmus milk culture: unchanged.
(l4) Formation of ammonia: not derivable from peptone.
( 15) Utilization of cellulose: none.
(16) Methylene blue reduction: positive.
(17) Pigment formed: Lemon yellow, water insoluble,
not changed colour of medium.
(18) Fermentation of various sugars: acid production with quick decomposition from glucose, fructose, su-
crose, maltose, and mannose; acid production with late decomposition from threhalose, inositol, and aesculin; no acid production from lactose, xylose, arabinose, rhamnose, rafiinose, galactose, glycerol, adonitol, mannitol, dulcitol, sorbitol, salicin dextrin, starch, inulin and blycogen; no gas production from any sugars.
(l9) Actiological properties: not germ of guinea pig or mouth disease.
(20) Nutrition-requesting nature: biotin-requesting and cystine.
(21) Observed lactic acid in a medium in a stand culture containing glucose in its medium.
In order to make species different from said Microbacterium ammoniaphilum No. 2001 from L-glutamic acid producing bacteria, the inventors of this strain have already obtained several strains which have close resemblance to microbiological characteristics, e. g. out of sugar utilization by No. 2109 strain, acid production from escrin is different and the form of agar flat colony is a little different, but other properties are exactly the same as those of No. 2001 strain. It is considered that L-glutamic acid producing bacteria belonging to Microbacterium ammoniaphilum' are spread widely in the natural world. It is crystal clear in view of the abovesaid characteristics of Microbacterium ammoniaphilum in accordance with Bergeys Manual of Determinative Bacteriology (1957) 7th ed. published by the Society of American Bacteriologists that the strain Microbacterium ammoniaphilum belonging to the order Eubacteriales, because the strain is a bacterium of which characters are the following, i.e., gram strain: positive, spore formation: none, acid-fast strain: negative, hight pleomorphism, angular and palisade: observed clearly. From the fact that among the families of aforesaid known L-glutamic acid producing microorganisms, the family Micrococcuseae is coccoi or egg-shaped having no thermal-resistance, the family Brevibacteriace-ae has no pleomorphism and no thermal-resistance and the family Baccilluseae has spore formation, it is concluded that the strain of the invention belongs to none of the above families and that the strain of the invention should belong to the family Corynebacteriaecae. And further, it is clearly concluded from the following facts (1)-(7) in careful comparison with genuses belonging to the family of Corynebacteriaecae cited in Bergeys Manual that the strain of the invention should belong to the genus Microbacterium.
(1) It is denied that the strain of the invention belongs to the genus Listeria because of its non-motility.
(2) Also denied that genus Erysipelothrix because its catalase reaction is positive and the strain grows in aerobic condition.
4 remarkable ability of producing and accumulating L-glutarnic acid by culturing the strain under aerobic conditions in a medium containing carbohydrate, nitrogen source and other nutrients.
In general, in cases where L-glutamic acid is attempted to be produced by fermenting cane molasses with L-glutamic acid-producing bacteria, if a mere nutrient culture medium having molasses as the main component is used, the object cannot be accomplished because of biotin active element present in the cane molasses. This is the same even in the case of M icrobacterium ammonaphilum having the above said property in this invention.
So far, many attempts were made, and some succeeded, in respect of the L-glutamic fermentation in a nutrient culture medium consisting of such carbohydrate materials. As a typical method thereof, there is the invention applied for by Merck & Co. (U.S. Patent No. 3,080,297). The technical essence thereof is a method of adding an inhibitor selected from among the antimicrobial agents consisting mainly of antibiotics to a culture medium.
However, even with the method mentioned above, it was found dfiicult to obtain an effect sufficient for industrial practice. Based on this fact, the present inventors made various studies of the action of chemical substances to be added to a culture medium or to the medium under cultivation they have derived this invention, which is, particularly, constructed of a novel technique of adding different chemical agents in two steps to a culture medium. The efifect of the two-step addition is shown in Table 1 below in respect of the case of several surface active agents.
TABLE 1 1 Step Addition 2 Step Addition Name of Surface Active Agents Amount of Amount of Amount Time of Ad- L-Clutamic Amount Time of Ad- L-Glutamic added (g./dl.) dition (hrs) Aznd paired added {g.ldl.) dition (hrs.) Acid formed 8- I11 (mg/m1.)
Tween 0- 2 0 0. 0
Catiolita SA- ..i i 0. 0g 3 Emanon 3115 0.2 0 u 5 0.10 0
ficetammeg 6i O. 01 8 0 minone 2 5 0 0.02 Cation A.B ..l 3 i 0. 01 3 3 (3) Further denied the genus Cellulomonas because the strain has non-utilization of cellulose.
(4) Still further denied the genus Arthrobacter because morphological'change in life cycle and change of gram stain in each age of fermentation are not observed.
(5) Etiological nature and high nutrient-requesting nature as in the genus Corynebacterium are not observed, but the nutrient-requesting nature of the strain is higher than the same nature of the genus Cellulomonas and Arthrobactor (both are soil microorganisms), that is, the strain is cystineand biotin-requesting.
(6) The strain produces lactic acid in a medium in a stand culture.
(7) The strain bears up against heating for 30 minutes at 70 C. or for 15 minutes at 72C.
As regards species, the species of the invention differs from both Microbacterium lacticum and Microbacterium flavum which are described as species belonging to the genus Microbacterium in Bergeys Manual, in view of the difference in the starch and maltose decomposition natures which-are considered as the identification key of the both species. And further, both Microbacterium lacticum ATCC No. 8180 and Microbacterium flavum ATCC No. 10340 which have been deposited as a standard strain belonging to the genus Microbacterium at the American Type Culture Collection and have been given the numbers, have no ability of producing L-glutamic acid. On the contrary, the strain of the invention has a Composition of culture medium for the main fermentation:
Cane molasses 9 g., urea 1.2 g., KH PO 0.1 g. per dl. Composition of cane molasses used:
Total carbohydrate 54.47 g./dl., dilect reducing sugar 10.28 -g./dl., biotin 98.6 mg./ g. Culture condition: 30 C., 48 hrs., shaking culture.
As shown in Table 1, the method of this invention based on the two-step addition system, as compared with the hitherto-known methods based on the one-step addition system, makes it possible to appreciably increase the formation of L-glutamic acid and, what is more, to make the amount of chemical agents to be added small, and, therefore, there is the advantage that the method of this invention can be worked economically on a commercial basis.
In the practice of this invention, chemical agents are added in two steps to a culture medium or to the medium under cultivation. As the chemical agents to be added in the first step, there are non-ionic surface active agents, which are selected from the group consisting of esters of polyoxyethylene sorbitan fatty acid, polyoxyethylene fatty acid, etc. and polyoxyethylene alkylamine. The chemical agents to be added in the second step are selected from the group of compounds such as surface active agents and 5 antibiotics. The use of chemical agents having the components shown below is particularly effective.
Components of the chemical agents to be added in the first step Polyoxyethylene sorbitan monopalmitate Polyoxyethylene sorbitan monostearate Polyoxyethylene monostearate Polyoxyethylene monopalmitate Polyoxyethylene alkylamine, etc.
Components of the chemical agents to be added in the econd step Lauryl amine, Stea-ryl amine, palmityl amine, alkyl trimethyl ammonium chloride, alkyl dimethyl benzyl ammonium chloride, penicillin, erythromycin, leucomycin, synthetic penicillin derivative, streptomycin, etc.
Of these chemical agents, those which are used in the first step are added within several hours after commencement of culture, that is, at the time when the difference shows -0.6 between the optical density, as in the case in which the twenty-times diluted culture broth is measured with a wave length of 655111, by using an ordinary photoelectric colon'meter with a 10 mm. cell, and the optical density at the time the culture is commenced. And, those which are used in the second step are added after lapse of more than one hour from the time the first component was 'added. The above-mentioned difference in optical density at this time is preferably 0.4-1.0
The molasses referred to herein is cane molasses.
The strain used in this invention, a typical one of which is ATCC 15354 strain, has several color mutants, which have the same characteristic features in taxology as those mentioned above. Accordingly, the strain which is made the objective of this invention is fully effective, regardless of whether its mutant is natural or artificial.
Hereunder, the method of this invention is explained with Working examples, which examples, however, are just several of those carried out by using Microbacterium ammoniaphilnm' ATCC 15354 strain and do not restrict this invention in any way whatsoever.
EXAMPLE 1 v G/dl. Cane molasses (as total carbohydrate) 7 KH SO 0.2 MgSO '7H O 0.05 MnSO -4H 0 0.0005 (NHQ SQ, 0.05
As the first-component surface active agent, one having polyoxyethylene monopalmitate as the main component was. selected and, When the optical density of the culture medium measured by the aforesaid method was 0.3, i.e. after about 5 hours from the time the culture was commenced, it was added to the culture medium so that the concentration thereof became 0.1 g./dl. And, as the second-component surface active agent, one having lauryl amine as the main component was taken up and, in the 6th hour after commencement of culture when the optical density became 0.55, it was added to the culture medium so that the concentration thereof became 0.025 g./dl.
Also, the pH of the culture medium under cultivation was adjusted to 7-8 with ammonia gas. While the culture temperature was being maintained at 30 C., about 2.6 l. of a liquid of cane molasses having a carbohydrate concentration of 50 g./dl. was supplied from the 12th hour after commencement of culture so that the concentration of the remaining carbohydrate became 1 g./d1., and the culture was carried out for 36 hours. In the culture medium, there was observed the accumulation of L- glutamic acid with a concentration of 7.85 g./dl. The total amount of L-glutamic acid formed was 1015 g. and the amount of carbohydrate used was 1989 g.; that is, the rate of yield was 51%.
Against this, when the second component was not used, the concentration of L-glutamic acid was 1.85 g./dl., and the total amount of L-glutamic acid formed was only 225 g. After completion of culture, 795 g. of coarse L-glutarnic acid crystals was obtained by the usual method from the former fermentation liquid.
EXAMPLE 2 The culture was carried out in the same way as in Example 1 by using the same Microbacterium ammoniaphilum ATTCC 15354 as in Example 1. However, the main fermentation culture medium used was of the following composition.
Composition of the main fermentation culture medium:
G./dl Cane molasses (as total carbohydrate) 7.0 KH PO 0.2 MgSO., 7H O 0.05 (NH SO 0.05 MnSO -4H O 0.0005
The pH adjustment and the supply of carbohydrate were carried out in the same way as in Example 1, but as the first-component surface active agent, one having polyoxyethylene sorbitan monopalmitate as the main component was used; it was added to the culture medium so that the concentration thereof became 0.1 g./d*l. in the 4th hour after commencement of culture when theoptical density of the culture medium was 0.3. Also, as the second component, a surface active agent'having lauryl amine as the main component was added to the culture medium so that the concentration thereof became 0.025 g./dl. when the optical density was 0.60, i.e. after lapse of 5.5 hours from the time the culture was commenced, and the culture was continued for 36 hours.
In the culture medium, there was observed the accumulation of L-glutamic acid with a concentration of 7.63 g./dl. The total amount of L-glutamic acid produced was 958 g. Against this, when the second component was not added, the concentration of L-glutamic acid was 1.12 g./dl. and the total amount produced was only g.
EXAMPLE 3 1.5 ml. of the culture broth pre-cultured by using the same Microbacterium ammoniaphilum ATCC 15354 as in Example 1 was inoculated into 75 ml. of the culture medium having the following composition placed in a 500 ml. shaking flask.
d Composition of the main fermentation culture merum:
In the 6th hour after commencement of culture, a surface active agent having palmityl amine as the main component was added as the second component in a ratio of 0.015 g./dl., and the culture was carried out for 48 hours at 30 C. In the culture medium, there was observed the 7 accumulation of L-glutamic acid with a concentration of 3.2 g./dl. On the other hand, when the second component was not added, there was the accumulation of L- glutamic acid with a concentration of only 1.5 g./dl.
As the second component, in the 6th hour aftercornmencement of culture, a surface active agent having benzalkonium chloride as the main component was added at a ratio of 0.01 g./dl. to the culture medium. In the culture However, the analytical values of the cane molasses medium after 48 hours, there was observed the accumulatreated with ammonium phosphate used herein were as tion of L-glutamic acid with a concentration of 2.7 g./dl. follows: against this, when the second component was not added, there was observed the formation of L-glutamic acid with TQtal carbohydrate 1607 a concentration of only 0.8 g./ d1. Dlrect reducing sugar g./dl 5.20 Biotin 10o cc 33.3 EXAMPLE 6 EXAMPLE 4 Microbacterium am'm orviapl ilum ATCC 15354 pre-cultured for 24 hours at 30 C. in a boulllon agar slant was h h-Y C0101 mutant of obfilctenum inoculated into a seed culture medium consisting of the momaphllllm ATCC 15354 Wa$ cu1mred 1h 3 500 following composition, and shake-cultured for 28 hours shaking flask in the same way as in Example 3. However, at 30 th ultu medium used was of the followin corn osij re g p Corn steep llquer ml./dl 4.0 Amino acid liquid -ml /dl 40 Composition of the main fermentation culture me- KH PO r r g 2 4 mm. MgSO -7H O g./dl 0.1 Cane molasses (as total carbohydrate) 7.0 2 m1. thereof was inoculated into 100 ml. of the main KH PO 0.2 culture medium having the following composition pre- MgSO -7H O 0.05 pared in a 500 ml. shaking flask, and, while the pH under Urea 1.5 cultivation was being maintained at around 7 with urea MnSO -4H O 0.0005 water, the shaking culture was continued at C. Polyoxyethylene monostearate 0.2 G ml The culture was carried out on a shaker for 48 hours. Cane molasses 10 In the 6th hour after commencement of culture, a sec- 30 2 4 ond-com'ponet surface active agent having alkyl trimethyl polyoxyethylehe sorhltan monopalmltate (Tween ammonium chloride as the main component was added 02 to the culture medium so that the amount thereof became In the 8th hour ft commencement f culture, various g In the culture h h after f i there antibiotics were added. The culture was further continued, was observed the accumulatlon of L-glutamlc ac1d with a 35 and ft 43 hours l i i the amount f hn i c t p g/dlacid in the culture medium was calculated by the mano- Agalhst this: When the Second cofhpoheht was q metric method of detecting the CO generated in the f Was ohsefved the formation of L-ghltflmlc enzymatic dicarboxylation of L-glutamic acid. The red Wlth a cohcehtl'atlon of y sults are shown in Table 2. The reference in the table The analytical values of the cane molasses used herein 4 shows the results of production tests i the above-menwere as follows: tioned culture medium without, however, Tween 40.
TABLE 2 Method of This Invention Reference Antibiotics Amount L-GA Amount L-GA Added Formed, Added Formed, mg./ml. mgJml.
Penicillin G 5 25 s 20 U/ml 15.0 Phenoxypenieillin 5 U/rnl 21.4 20 U/ml 14.6 Penicillin v. 5U/rul 25.9 20 U/ml 15.1 Tetracyelin 5mog./ml 14.7 10 mcg./ml 2.4 Erythromyein lmcgJml. 14.2 10 mcgJmL- 5.0 Leuicomycin 0.5 meg/ml. 18.8 5mcg./ml 7.7
Total carbohydrate percent 49.65 EXAMPLE 7 Direct reducing sugar do Biotin 100 g EXAMPLE 5 Microbacterium: ammoniaphilum ATTC 15354 was shake-cultured in a 500 ml. shaking flask in the same way as in Example 3. However, the main fermentation culture medium used was of the following composition:
amine as main component 1 g. of stearylamine acetate (Catiolite 500 ml. of the bacterial seed of Microbacterium ammoniaphilum ATCC 15354 obtained in the same way as in Example 6 was inoculated into 10 l. of the culture medium (charged in 20 l. jar fermenter) for the main fermentation having the following composition:
G./dl.
Cane molasses (as total carbohydrate) l0 KH PO 0.1 Polyoxyethylene sorbitane monopalmitate (Tween In the 9th hour after commencement of culturing 3.0 SA) was added. The culture was carried out under submerged aerobical conditions while adjusting the pH to 8.0 with ammonium liquid during culturing. The amount of L-glutamic acid ac cumulated in the cultue medium after 48 hrs. was 46.0
mg. per m1. Incidentally, L-glutamic acid can be collected from the culture broth in the same way as in Example 1.
EXAMPLE 8 Like in Example 6, Microbacteriwm ammoniaphilum ATCC 15354 was shake-cultured at 30 C. in a seed culture medium, and 500 ml. thereof was inoculated into a 20 l. jar fermenter containing l. of the culture medium for main fermentation having the following composition:
Cane molasses treated with ammonium phosphate (as total carbohydrate) 10 KH PO 0.1 MgSO -7H O 0.05 Polyoxyethylene alkylamine (Aminon 295) 0.05
Total carbohydrate g./dl 16.07
Direct reducing sugar g./dl 5.20
Biotin mcg./dl 33.3
What is claimed is:
1. In the method for preparing L-glutamic acid by fermentation of carbohydrate materials by culturing microorganisms belonging to Microbacteria ammonimolasses as the main component, an improvement comprising carrying out said fermentation in the presence of a nonionic surface active agent selected from the group comprising polyoxyethylene sorbitan monopalimitate, polyoxyethylene sorbitan monostearate polyoxyeth ylene monostearate, polyoxyethylene monopalmitate and polyoxyethylene alkylamine, subsequently adding a chemical agent selected from the second group comprising lauryl amine, stearyl amine, palmityl amine, alkyl trimethyl amine chloride, benzalconium chloride, penicillin, erythromycin, leucomycin streptomycin to the culture medium, continuing the culture aerobically, thereby forming and accumulating L-glutamic acid in the culture medium and isolating and collecting the same.
2. A method as defined in claim 1, wherein a nonionic surface active agent is used -as the component of the culture medium.
3. A method as defined in claim 2, wherein a compound selected from the group consisting of ionic surface active agents and antibiotics is added during the time the growth of microbacteria has reached from the middle to the last period of the log. phase.
References Cited UNITED STATES PATENTS 3,080,297 3/1963 Phillips et a]. 195-47 3,164,531 1/1965 Okada et al. 195-47 FOREIGN PATENTS 683,022 3 /1964 Canada. 683 ,023 3 1964 Canada.
A. LOUIS MONACELL, Primary Examiner.
philum in a nutrient culture medium containing cane L. M. SHAPIRO, Assistant Examiner.
Claims (1)
1. IN THE METHOD FOR PREPARING L-GLUTAMIC ACID BY FERMENTATION OF CARBOHYDRATE MATERIALS BY CULTURING MICROORGANISMS BELONGING TO MICROBACTERIA AMMONIPHILUM IN A NUTRIENT CULTURE MEDIUM CONTAINING CANE MOLASSES AS THE MAIN COMPONENT, AN IMPROVEMENT COMPRISING CARRYING OUT SAID FERMENTATION IN THE PRESENCE OF A NONIONIC SURFACE ACTIVE AGENT SELECTED FRO THE GROUP COMPRISING POLYOXETHYLENE SORBITAN MONOPALIMITATE, POLOXYETHYLENE SORBITAN MONOSTEREAT POLYOXYETHYLENE MONOSTEARATE, POLYOXYETHYLENE MONOPALMITATE AND POLYOXYETHYLENE ALKYLAMINE, SUBSEQUENTLY ADDING A CHEMICAL AGENT SELECTED FROM THE SECOND GROUP COMPRISING LAURYL AMINE, STEARYL AMINE, PALMITYL AMINE, ALKYL TRIMETHYL AMINE CHLORIDE, BENZALCONIUM CHLORIDE, PENICILLIN, ERYTHROMYCIN, LEUCOMYCIN STREPTOMYCIN TO THE CULTURE MEDIUM, CONTINUING THE CULTURE AEROBICALLY, THEREBY FORMING AND ACCUMULATING L-GLUTAMIC ACID IN THE CULTURE MEDIUM AND ISOLATING AND COLLECTING THE SAME.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3399114A (en) * | 1964-08-22 | 1968-08-27 | Asahi Chemical Ind | Process for producing l-glutamic acid by using bacteria |
EP0079792A3 (en) * | 1981-11-13 | 1983-11-09 | Kyowa Hakko Kogyo Co., Ltd | Process for production of urease |
FR2612937A1 (en) * | 1987-03-27 | 1988-09-30 | Ajinomoto Kk | New microorganisms and process for producing glutamic acid using these microorganisms. |
US5250434A (en) * | 1987-03-27 | 1993-10-05 | Ajinomoto Co., Inc. | Microorganisms for production of glutamic acid |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3080297A (en) * | 1960-07-11 | 1963-03-05 | Merck & Co Inc | Production of glutamic acid |
CA683023A (en) * | 1964-03-24 | Asahi Kasei Kogyo Kabushiki Kaisha | Process for producing l-glutamic acid by fermentation | |
CA683022A (en) * | 1964-03-24 | Tsuruo Isao | Method of producing l-glutamic acid by fermentation | |
US3164531A (en) * | 1961-10-19 | 1965-01-05 | Ajinomoto Kk | Process for preparing l-glutamic acid |
-
1964
- 1964-09-18 US US397629A patent/US3338793A/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA683023A (en) * | 1964-03-24 | Asahi Kasei Kogyo Kabushiki Kaisha | Process for producing l-glutamic acid by fermentation | |
CA683022A (en) * | 1964-03-24 | Tsuruo Isao | Method of producing l-glutamic acid by fermentation | |
US3080297A (en) * | 1960-07-11 | 1963-03-05 | Merck & Co Inc | Production of glutamic acid |
US3164531A (en) * | 1961-10-19 | 1965-01-05 | Ajinomoto Kk | Process for preparing l-glutamic acid |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3399114A (en) * | 1964-08-22 | 1968-08-27 | Asahi Chemical Ind | Process for producing l-glutamic acid by using bacteria |
EP0079792A3 (en) * | 1981-11-13 | 1983-11-09 | Kyowa Hakko Kogyo Co., Ltd | Process for production of urease |
FR2612937A1 (en) * | 1987-03-27 | 1988-09-30 | Ajinomoto Kk | New microorganisms and process for producing glutamic acid using these microorganisms. |
US5250434A (en) * | 1987-03-27 | 1993-10-05 | Ajinomoto Co., Inc. | Microorganisms for production of glutamic acid |
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